Method of rotational molding using a resin blend and the resulting molded objects

ABSTRACT

A method for making rotationally molded objects using resin blends. The resin blend comprises resin pellets and an amount of ground resin particles sufficient to yield rotomolded objects having desirable impact strength and other strength characteristics. Preferably, the resin blend comprises of from about 20% to about 30% by weight of ground resin particles. In addition, resin blends can be used to produce colored objects by rotational molding techniques.

This application claims the benefit of U.S. Provisional Application No. 60/104,507 filed on Oct. 16, 1998.

FIELD OF THE INVENTION

This invention relates to a method of rotational molding using a unique resin blend and to the resulting molded objects.

BACKGROUND OF THE INVENTION

Rotational molding is, in theory, a very straightforward process. To make an object using rotational molding, all that is required are: (1) a mold to hold the material in the configuration desired when the processing is complete; (2) a source of heat to melt the resin or plastic under control conditions; (3) a machine to distribute the material uniformly over the surface of the mold; and (4) a method of cooling the resin under controlled conditions.

There are several advantages which may be derived using rotational molding. The tooling costs are economical and a hollow, one-piece object results which is virtually stress-free. Uniform wall thicknesses can be provided, and there is substantial design flexibility, allowing molding of hollow, one-piece objects ranging from relatively small objects to intricate designs and to large and complex shapes.

Common rotationally molded products include, as illustrative examples, shipping drums, storage tanks and receptacles, material handling bins, and housings. Consumer products made using rotational molding range from furniture to toys and to marine accessories.

However, there are a variety of problems, difficulties and/or complications involved when using rotational molding. One significant problem derives from the process itself. The resin which is the standard commercially available is provided in relatively large-sized particles, typically in the form of pellets. The current result is that resin producers typically manufacture resins with a pellet size ranging from 35 to 60 pellets/gram. As hereinafter discussed, particles of this size do not process well given the processes currently being used by rotational molders. Accordingly, such relatively large pellets are ground to provide powders ranging from 22 mesh up to about 35 or even 50 mesh. The grinding processes involved typically result in a relatively wide bell-shaped particle distribution curve. In the rotomolding cycle, the smaller ground particles melt first, much like ground ice melts faster than ice cubes.

While such finely ground particles are widely used in the rotomolding process to achieve this faster melting quality, the use of such ground particles presents several problems. The particle size distribution achieved following grinding varies widely from one grinder to another. Indeed, sometimes the distribution curve will vary significantly even when the same grinder is used, such as, for example, which can occur when the mechanical set-up conditions are altered slightly. This variation in the particle size distribution will effect the delivery system in the rotomolding process which can cause variations in the wall thickness of the object being molded. Further, the grinding process adds not only significant expense, but can lead to inventory problems simply because of the volume of resin needed to be ground.

Still further, and importantly, the fines in such ground resin can create processing and housekeeping problems, simply due to the level of dust involved. Such resulting dust can likewise create a potential safety issue.

Yet, despite the continuing need for a solution to these very real problems, no solution exists insofar as the present inventor is aware. Rather, the resin source used in rotomolding continues to be ground particles.

SUMMARY OF THE INVENTION

In general, the present invention is predicated on the discovery that a resin blend capable of achieving rotationally molded parts having impact strength and other characteristics, similar to that achieved with ground resin particles, can be obtained by eliminating much of the ground resin particles previously considered essential. More particularly, it has been found that rotationally molded parts having adequate processing and strength and other product characteristics can be obtained utilizing a blend of resin pellets in the size range obtained from the resin manufacturer while utilizing only a minor amount of ground particles.

Thus, as one example, when using a rotomold grade of polyethylene, rotomolded parts having only 20% to 30% ground particles achieve low temperature impact strength characteristics essentially the same as those achieved with a rotomolded part made entirely from ground particles. This is particularly surprising, perhaps evidencing some synergistic processing and/or other properties, in view of the dramatic drop-off in properties that result when the ground particle component is reduced to 10% or less.

The present invention provides a method of rotational molding using a resin blend which avoids the problems of prior rotational molding techniques that employ ground resin. These and other advantages of the present invention, as well as additional inventive features, will be apparent from the description of the invention provided herein.

DESCRIPTION OF THE DRAWINGS

FIG. 1 is a plot of the air temperature profile in a uniaxial rotomolding machine as a function of time for various resins.

FIG. 2 is a graph showing the low temperature impact resistance of rotomolded objects by plotting main failure energy for various powder concentrations in the resin blend used to produce the rotomolded objects.

FIG. 3 is a graph showing the normalized (for unit thickness) low temperature impact resistance of rotomolded objects by plotting main failure for various powder concentrations in the resin blend used to produce the rotomolded objects.

FIG. 4 is a stress versus strain curve of rotomolded objects obtained using various resin blends.

FIG. 5 is a graph showing the tensile strength of rotomolded objects obtained using various resin blends.

FIG. 6 is a graph showing the percent elongation at break of rotomolded objects obtained by various resin blends.

DETAILED DESCRIPTION OF THE INVENTION

Typically, resins such as LLDPE resins (linear low-density polyethylene) are currently manufactured in a standard commercial pellet count of about 35 to 60 pellets/gram, as previously noted. While such pellets may be utilized to create rotationally molded parts, it has been found that such relatively large sized pellets will provide undesirable properties for direct use in rotationally molding, including the fabrication of composite laminates because of the melting and coalescence characteristics of such larger pellets. More particularly, composite laminates can be molded using different polymers or the same polymer with different physical properties and/or characteristics. The pellet size affects the ability of the polymer to melt out and achieve optimum particle coalescence. The molding process, including the selection of polymer having an appropriate particle size, is intended to achieve optimum adhesive and physical properties both within and between the composite laminate materials. However, as will be discussed hereinafter, the present invention utilizes a blend comprising predominantly such resin pellets.

Any type of resin used in conventional rotational molding may be utilized. The particular resin selected will be determined by the requirements for the object or part being rotationally molded. Currently, the most common resin used is polyethylene. Many types of polyethylene are commercially available, with a wide range of properties and all may be used. In general, the types of polyethylene available can be described as linear low-density polyethylene, low-density polyethylene, medium-density polyethylene, and high-density polyethylene. Still further, each material type is manufactured using unique technology to achieve desired material physical characteristics and properties. Examples of these are hexene, butene, and metallocene molecular chains used in resin technologies.

In addition, other polyolefins are known and may be used. Further, ethylene-vinyl acetate resins can be used.

Still further illustrative examples of other types of resins useful in the method of this invention include polycarbonates, nylons, polyvinylchlorides, and polyesters. Additional useful resins include ABS, acetals, acrylics, cellulosics, epoxies, fluorocarbons, phenolics, polystyrenes, polyurethanes, SAN polymers, and silicone polymers.

Typically, any useful colorants may be used to provide the desired colors for the particular product being molded. Any heat stable and unreactive colorants known and available for use for the particular resins may be employed. As illustrative examples, virtually any color can be provided, ranging from white to yellow, red, orange, green, burgundy and black.

Illustrative examples of useful colorants include titanium dioxide, carbon black, iron oxide, ultramarine blue, cadmium sulfide, phthalocyanine green, phthalocyanine blue, chromium oxide, quinacridone red, anthraquinone and perinone dyes. The amount of colorant used can be varied as is necessary to provide the desired color. In general, the amounts used will vary from about 0.1% to about 3%.

In addition, any other additives may be employed as is optional ingredients as is known from conventional rotational molding. For example, it may be desirable to provide a tackifying agent to, in effect, allow the colorant to coat the resin particles. Many suitable tackifying agents are known, and white mineral oil is useful. The amount utilized should be only at the level desired to provide the requisite tackifying effect to avoid any possible undue adverse effects on the physical properties of the molded article or object. Other optional additives include dispersing agents, UV stabilizers and/or antioxidants in the amount that are known to provide the desired effects.

Pursuant to the present invention, and in marked contrast with currently used ground resin charges, the present invention utilizes a resin blend comprising predominantly resin pellets in the size provided by the resin manufacturer together with a minor amount of ground resin particles. The amount of ground resin need only be that level sufficient to yield rotomolded parts having the desired impact strength and other strength properties. The amount of ground resin particles needed to provide the desired strength characteristics can vary depending upon the resin and the size of the resin pellets available. When the proportion of the ground resin component is present at too low a level, a significant drop-off in the desired properties will often result. On the other hand, due to the problems created by utilizing ground particles, there is no functional reason to employ levels of ground resins in excess of those needed to satisfy the processing and molded part characteristics desired for the particular application.

To this end, rotomolding grade resins, particularly polyolefin resins, such as polyethylene, can achieve suitable processing and product characteristics by employing only about 20% to 30% or so of the ground resin by weight, the percent being based upon the total weight of the blend. This ground resin range should be useful where the resin pellets employed range from about 35 to about 60 pellets per gram or so. Preferably, the ground resin particles are present in an amount of about 30% by weight based on the total weight of the resin blend. It is expected that the level of ground resin needed will increase somewhat, with larger-sized pellets. As may be appreciated, the pellet size, if desired, can be above or below the typical 35 to 60 range. Indeed, by adjusting the pellet size it may be desirable to optimize the desired characteristics of the molded object.

The reasons for what are considered to be the surprising results achieved are not fully understood. These results may evidence a complex relationship involving such processing aspects as coalescence mechanisms resulting from what perhaps may be considered as a zero shear rotomolding fabricating process as the resin blend undergoes the melting process and is transferred in molten form to the inner wall of the mold.

In any event, the advantages of the present invention are varied and substantial. First of all, the use of the present invention eliminates the necessity of having to grind the vast majority of the resin required to make a rotomolded part, offering a significant cost reduction for the molder. The housekeeping expenses incurred by rotomolders are significantly reduced because of the lessened volume of dusty powder that needs to be handled. Still further, and importantly, the uniform particle distribution of the resin pellet typically available from the resin manufacturer produces what is considered to be a synergistic delivery mechanism which allows molding of objects of a more uniform wall thickness than can be easily obtained with the use of the conventional ground resin charge.

Another important aspect of the present invention concerns the significant improvements that can be obtained for rotomolded objects that are colored. At present, the industry pigments resins in one of two manners. One approach is to utilize precolored material. More particularly, the polymer is colored in the extrusion compounding operation and is thereafter extruded into a pellet configuration that is later converted into a powder by the grinding process. The other approach is to use dry color pigments added to ground natural resin during the rotomolding process.

Pursuant to one aspect of this invention, an alternate method of achieving a colored rotomolded object is provided which is not considered achievable at present. To this end, the present invention contemplates increasing the level of pigmentation in the ground resin component of the resin charge so as to provide increased opacity. In this fashion, the rotomolder should be able to utilize natural resin pellets, viz., pellets which have not been precolored. With this approach, a considerable reduction in cost can be achieved. Even further, the present invention permits rotomolders presently using dry pigments to color their resins with an alternate method of coloration at a cost comparable to the present cost of dry coloring. Additionally, the use of the present invention to achieve a colored, rotomolded object, in contrast to current dry coloring techniques, reduces the housekeeping expense and eliminates cross-color contamination created by airborne dry pigment particles.

The following examples further illustrate the present invention but, of course, should not be construed as in any way limiting its scope.

EXAMPLE 1

This Example demonstrates the characteristic inside air temperature profile in a uniaxial rotomolding machine for both a 100% powder resin and a 10% powder/90% large pellet resin blend used according to the method of the present invention.

A square mold was filed with 100 g of preweighed polymer. A uniaxial rotomolding machine was set to rotate at 4 rpm. After the mold rotation began, an infra-red oven (preheated to 408° C.) was placed over the mold. The inside air temperature was then recorded over a series of timed intervals. The heating cycle was stopped (i.e., the oven was removed) when the inside air temperature reached 239° C. (expect for the 100% powder resin). The plots of the inside air temperature versus time for both the 100% powder resin and 10% powder/90% large pellet resin blend are shown in FIG. 1. As can be seen, the heating cycle was completed earlier when the 10% powder/90% large pellet resin blend was used.

EXAMPLE 2

This Example compares the mechanical properties including impact resistance and tensile strength of rotomolded objects made using resin blends according to the method of the present invention as compared to such impact resistance and tensile strength of rotomolded objects produced using other resins.

Six rotomolded samples were prepared by rotomolding polyethylene resins and resin blends on a computer controlled M20 FSP Clamshell machine. The temperature and residence time for the gas-fired oven were set at 310° C. and 3 minutes, respectively.

The large pellets of polyethylene resin used to prepare Samples 1-5 are made of a rotomolding grade polyethylene resin identified as Lot # MP 635-661. The micropellets used to prepare Sample 6 are made of an injection molding grade polyethylene resin identified as Lot # LL-6407. The composition of the resin blend used to produce these samples and the sample densities are shown in Table 1 below:

TABLE 1 Sample Resin Formulation Density (g/cc) 1 100% powder 0.936 2  10% powder 0.936  90% large pellet 3  20% powder 0.936  80% large pellet 4  30% powder 0.936  70% large pellet 5 100% large pellet 0.936 6 100% micropellets 0.935

The rotomolded objects in Samples 1-5 were subjected to a low temperature dart impact test. This impact test, also known as the A.R.M. method, determines the energy required to cause failure of the rotomolded part using a free falling dart. Samples of the rotomolded parts were placed into a sample holder with the inside surface of the part facing down. The dart was raised to a height expected to cause half of the samples to fail. The graph of main failure energy for Samples 1-5 is shown in FIG. 2. The graph of main failure energy normalized for the average sample thickness in Samples 1-5 is shown in FIG. 3. Sample 6 prepared from an injection grade polyethylene resin had no impact strength.

As can be seen in FIGS. 2 and 3, equivalent low impact strength characteristics are achieved using a resin blend containing 20% or 30% powder when compared to a molded part made entirely with ground resin particles (i.e., 100% powder). A substantial drop off in impact strength was observed when the level of ground resin particles was reduced to 10% or eliminated altogether (i.e., 100% large pellets). In addition, the rotomolded object prepared from a 30% powder blend (Sample 4) was observed to have a nice surface finish as compared to objects made using resins with decreased ground powder content which has uneven surfaces with holds.

The rotomolded objects of Samples 1, 4 and 6 were subject to a tensile strength analysis. The tensile strength (at yield), percent elongation at break and tensile stress (at break) for these objects are shown in Table 2 below:

TABLE 2 Tensile Percent Tensile Strength @ Elongation @ Stress @ yield break break Sample (MPa) (%) (MPa) 1 22.00 1148 21.55 4 21.35 1094 20.85 6 16.63 483 5.96

The plots of tensile stress versus strain for these three rotomolded samples are shown in FIG. 4. The tensile strengths at yield and at break for Samples 1, 4 and 6 which are set forth in Table 2 are likewise plotted in FIG. 5. The graph in FIG. 6 illustrates the percent elongation at break for rotomolded Samples 1, 4 and 6 as set forth in Table 2.

As can be seen from this tensile strength analysis, the rotomolded object produced by a 30% powder resin blend according to the present invention achieves tensile strength characteristics equivalent to those obtained using a conventional rotomolding charge, viz., 100% resin powder.

All of the references cited herein, including patents, patent applications, and publications, are hereby incorporated in their entireties by reference.

While this invention has been described with an emphasis upon preferred embodiments, it will be obvious to those of ordinary skill in the art that variations of the preferred embodiments may be used and that it is intended that the invention may be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications encompassed within the spirit and scope of the invention as defined by the following claims. 

What is claimed is:
 1. A resin blend composition for use in rotational molding comprising resin pellets and ground resin particles made of the same resin to yield a single-layered rotomolded object, wherein said ground resin particles are present in an amount of from about 20% to about 30% by weight based on the total weight of the resin blend composition.
 2. The resin blend composition of claim 1, wherein said ground resin particles are present in an amount of about 30% by weight based on the total weight of the resin blend composition.
 3. The resin blend composition of claim 1, wherein said resin pellets and ground resin particles are polyethylene.
 4. The resin blend composition of claim 3, wherein said resin pellets and ground resin particles are linear low-density polyethylene.
 5. A resin blend composition for use in rotational molding comprising resin pellets and ground resin particles made of the same resin to yield a first single-layered rotomolded object, wherein said ground resin particles are present in a sufficient amount such that the first rotomolded object has tensile strength characteristics substantially similar to a second rotomolded object produced from a resin composition containing 100% ground resin particles.
 6. The resin blend composition according to claim 5, wherein the tensile strength at yield of the first rotomolded object is about 20 mPa.
 7. The resin blend composition according to claim 5, wherein the percent elongation at break of the first rotomolded object is about 1100%.
 8. The resin blend composition according to claim 5, wherein the tensile stress at break of the first rotomolded object is about 20 mPa.
 9. The resin blend composition according to claim 5, wherein said ground resin particles are present in an amount of from about 20% to about 30% by weight based on the total weight of the resin blend composition.
 10. A resin blend composition for use in rotational molding comprising resin pellets and ground resin particles made of the same resin to yield a singe-layered rotomolded object, wherein the rotomolded object has a tensile strength at yield of about 20 mPa, a percent elongation at break of about 1100%, and a tensile stress at break of about 20 mPa. 